Rate-Based Model in Bubble Cap Batch Distillation Column - Salah S. Ibrahim
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Toimitus 15-21 arkipäivässä
30 päivän palautusoikeus
The dynamic behavior of trayed batch distillation column has been studied theoretically and experimentally. The experimental work was performed through using a batch distillation column consisting of eight bubble-cup trays. A zeotropic (nonazeotropic) system of Benzene, Toluene, and Ethylbenzene (B-T-EB) had been used. The theoretical study was performed through modeling that including of coupling mass and ... Täydellinen kuvaus
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Kuvaus
The dynamic behavior of trayed batch distillation column has been studied theoretically and experimentally. The experimental work was performed through using a batch distillation column consisting of eight bubble-cup trays. A zeotropic (nonazeotropic) system of Benzene, Toluene, and Ethylbenzene (B-T-EB) had been used. The theoretical study was performed through modeling that including of coupling mass and energy transfer between vapor and liquid phases so-called ¿Nonequilibrium (or Rate)-Based modeling¿. This study will be useful for researchers whose work on transport phenomena modeling.
Lisätietoja
| Kirjoittaja | Salah S. Ibrahim |
|---|---|
| Julkaisija | Scholars' Press |
| Julkaisuvuosi | 2017 |
| Kannen tyyppi | Pehmeäkantinen |
| EAN | 9783330651265 |